EP2239369A1 - Produit d'encollage du papier - Google Patents

Produit d'encollage du papier Download PDF

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Publication number
EP2239369A1
EP2239369A1 EP09157679A EP09157679A EP2239369A1 EP 2239369 A1 EP2239369 A1 EP 2239369A1 EP 09157679 A EP09157679 A EP 09157679A EP 09157679 A EP09157679 A EP 09157679A EP 2239369 A1 EP2239369 A1 EP 2239369A1
Authority
EP
European Patent Office
Prior art keywords
oil
size
paper sizing
sizing emulsion
paper
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP09157679A
Other languages
German (de)
English (en)
Inventor
Elisabeth Lackinger
Klaus Möller
Jürgen SARTORI
Leo Schmid
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kemira Oyj
Original Assignee
Kemira Oyj
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kemira Oyj filed Critical Kemira Oyj
Priority to EP09157679A priority Critical patent/EP2239369A1/fr
Priority to CA2756148A priority patent/CA2756148C/fr
Priority to US13/263,121 priority patent/US8512521B2/en
Priority to ES10717671T priority patent/ES2747791T3/es
Priority to MX2011010653A priority patent/MX2011010653A/es
Priority to EP10717671.1A priority patent/EP2417297B1/fr
Priority to RU2011141340/04A priority patent/RU2538957C2/ru
Priority to PL10717671T priority patent/PL2417297T3/pl
Priority to BRPI1016127A priority patent/BRPI1016127B1/pt
Priority to JP2012504042A priority patent/JP5737814B2/ja
Priority to CN2010800156170A priority patent/CN102388181B/zh
Priority to KR1020117026730A priority patent/KR101736413B1/ko
Priority to PCT/FI2010/050288 priority patent/WO2010116044A1/fr
Priority to AU2010233629A priority patent/AU2010233629B2/en
Publication of EP2239369A1 publication Critical patent/EP2239369A1/fr
Priority to CL2011002504A priority patent/CL2011002504A1/es
Priority to ZA2011/08224A priority patent/ZA201108224B/en
Withdrawn legal-status Critical Current

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Classifications

    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H21/00—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
    • D21H21/14—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties characterised by function or properties in or on the paper
    • D21H21/16—Sizing or water-repelling agents
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/20—Macromolecular organic compounds
    • D21H17/21—Macromolecular organic compounds of natural origin; Derivatives thereof
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H21/00—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
    • D21H21/14—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties characterised by function or properties in or on the paper
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/02—Material of vegetable origin
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/03—Non-macromolecular organic compounds
    • D21H17/05—Non-macromolecular organic compounds containing elements other than carbon and hydrogen only
    • D21H17/14—Carboxylic acids; Derivatives thereof
    • D21H17/15—Polycarboxylic acids, e.g. maleic acid
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/03—Non-macromolecular organic compounds
    • D21H17/05—Non-macromolecular organic compounds containing elements other than carbon and hydrogen only
    • D21H17/14—Carboxylic acids; Derivatives thereof
    • D21H17/15—Polycarboxylic acids, e.g. maleic acid
    • D21H17/16—Addition products thereof with hydrocarbons
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/62—Rosin; Derivatives thereof

Definitions

  • Sizing of paper is used to hinder penetration of water into the sheet. This repellence is needed for durability and other wished paper characteristics like printability.
  • sizing agents belong to the functional chemical group. Hydrophobation of the fiber can be achieved by a modification of the fiber constitution in the paper. Molecules which are able to attach to the fiber with one side and hinder the penetration of water with the other side are added to the furnish during the papermaking process. When paper is sized in this way it is called internal sizing.
  • the common sizing agents for neutral and alkaline sizing react with the hydroxyl groups of the cellulose, they are also called reactive sizes.
  • the most common used reactive sizes are alkyl ketene dimers (AKD) and alkenyl succinic anhydrides (ASA). While the first mentioned shows a reasonable hydrolytic stability the opposite is true for ASA. Consumption of reactive sizing agents is significantly lower than for the rosin sizes.
  • ⁇ -olefins need to be isomerized to form internal olefins. This means the double bond is shifted away from an outward position of the molecule.
  • MAA maleic acid anhydride
  • the prior production of the internal olefin is necessary due to the higher melting point of an ASA produced from ⁇ -olefin, which means the ⁇ -ASA would be solid at room temperature and this would make the application at paper machines quite difficult.
  • WO 03/000992 discloses a soybean derived product (PDS size) comprising pure fatty acids extracted directly from soybean oil.
  • WO 2006/002867 disclose yet another alternative sizing agent in the form of a dispersion comprising dispersed in water a sizing agent composed of a reaction product of maleic acid anhydride (MAA) and an unsaturated fatty acid alkyl ester, the sizing dispersion additionally comprising an aluminium compound such as aluminium sulphate, polyaluminium sulphate or polyaluminium chloride.
  • MAA maleic acid anhydride
  • an aluminium compound such as aluminium sulphate, polyaluminium sulphate or polyaluminium chloride.
  • CA 1 069 410 discloses the use of an emulsifying agent comprising a trialkylamine or ammonium hydroxide in combination with a sizing agent.
  • the sizing agent may be a maleated vegetable oil, maleated ⁇ -olefine, maleated fatty ester or AKD.
  • a paper sizing emulsion comprising a maleated vegetable oil size wherein at least 50% by weight of the total fatty acids of the triglycerides are monounsaturated.
  • the main constituent of a vegetable oil is triglyceride in which glycerol is esterified with three fatty acids.
  • the vegetable oil size of the present invention is emulsified in an aqueous solution.
  • At least 60% by weight, more preferably at least 70% by weight, and most preferably at least 80% by weight of the total fatty acids of the triglycerides are monounsaturated.
  • the vegetable oil of the maleated vegetable oil preferably originates from vegetable oil comprising rapeseed oil (including Canola oil), high oleic sunflower oil, high oleic safflower oil, olive oil or hazelnut oil or a mixture thereof.
  • rapeseed oil including Canola oil
  • high oleic sunflower oil high oleic safflower oil
  • olive oil or hazelnut oil or a mixture thereof high oleic sunflower oil is especially preferred.
  • Typical oleic acid contents of some suitable vegetable oils are as follows.
  • the paper sizing emulsion according to the present invention may additionally comprise a second size comprising an alkenyl succinic anhydride (ASA) size or a fatty acid anhydride (FAA) size or a mixture thereof.
  • ASA alkenyl succinic anhydride
  • FAA fatty acid anhydride
  • the fatty acid of the FAA size is preferably derived from tall oil, sunflower oil, rapeseed oil, soy bean oil, linseed oil or animal oil or a mixture of two or more of these oils.
  • the weight ratio of the maleated vegetable oil size to the second size is preferably from 1:9 to 9:1, more preferably from 3:7 to 7:3.
  • the second size comprises a mixture of the alkenyl succinic anhydride (ASA) size and the fatty acid anhydride (FAA) size.
  • ASA alkenyl succinic anhydride
  • FAA fatty acid anhydride
  • the paper sizing emulsion according to the present invention may additionally comprise an anionic or non-ionic emulsifier, such as a sulfosuccinate, e.g. sodium salt of di-octyl sulfosuccinate (Na-DOSS), or a fatty alcohol ethoxylate, e.g. tridecyl-alcohol ethoxylate.
  • an anionic or non-ionic emulsifier such as a sulfosuccinate, e.g. sodium salt of di-octyl sulfosuccinate (Na-DOSS), or a fatty alcohol ethoxylate, e.g. tridecyl-alcohol ethoxylate.
  • the amount of the emulsifier is preferably from 0.5 to 2 % by active weight of the sizing agent(s).
  • the paper sizing emulsion according to the present invention may additionally comprise a protective colloid such as polymer, starch, or another polysaccharide.
  • a protective colloid such as polymer, starch, or another polysaccharide.
  • Starch can be modified starch for example cationic starch.
  • maleated vegetable oils of the present invention is shown in following reaction scheme wherein one mole of a triglyceride having C 18:1 chains is reacted with one mole of maleic acid anhydride.
  • the maleated vegetable oil is obtained by reacting maleic acid anhydride with the vegetable oil in a molar ratio of maleic acid anhydride to the triglyceride of preferably at least 1:1, more preferably at least 2:1, and most preferably at least 3:1.
  • a molar ratio of maleic acid anhydride to the triglyceride of preferably at least 1:1, more preferably at least 2:1, and most preferably at least 3:1.
  • the reaction time is shortened and the content of residual oil decreases.
  • One benefit of the shorter reaction time is that fewer polymers are produced as the time the reaction mixture is held at high temperature is reduced.
  • the reaction temperature is typically 190-250 °C and the reaction time typically 2-81 ⁇ 2 h, preferably 31 ⁇ 2-81 ⁇ 2 h, and more preferably 5-7 h. Too long reaction times lead to the increase of the viscosity of the product.
  • the excess MAA is distilled off after reaction typically in temperature 120-140 °C and in reduced pressure for example in 10 mbar for
  • antioxidants are benzoquinone derivates, hydroquinone derivates, dialkylsulfoxide, acetylacetonate of a transition metal or acetylacetonate of a transition metal oxide. Additionally, boric acid or mixtures of boric acid and BHT can be used.
  • the concentration of the size(s) in the aqueous emulsion is preferable between 10% and 0.1 %, more preferably between 5% and 0.5%.
  • the emulsion Prior to the addition of the sizing emulsion of the invention into the fibre stock the emulsion can be diluted for example in the proportion 1 part of emulsion to 10 parts of water.
  • the emulsifier is dissolved in the size prior to the emulsification.
  • Additional agents conventionally used in paper manufacturing including aluminium salts such as aluminium sulphate or polyaluminium chloride and retention aids such as a cationic polymer may be added to the fibre stock.
  • emulsifiers are not necessary for these processes, but their addition leads to smaller particles and therefore is beneficial.
  • An especially preferred emulsifier is sodium di-octyl sulfosuccinate, because of its stability in cold maleated vegetable oils.
  • the present invention also relates to the use of a paper sizing emulsion as defined above or prepared by the above process for surface sizing or internal sizing of papers, such as various printing papers, magazine papers, newsprint papers and copy papers, and boards, such as packing boards and liquid packing boards.
  • Typical amount of size for papers, especially printing paper, and for boards is about 0.2 - 3 kg/t, preferably about 0.4 - 2.5 kg/t (active content/paper ton).
  • rapeseed oil 73.7kg rapeseed oil (oleic acid content 53.9%) was reacted with 16.3kg maleic acid anhydride (MAA) with the addition of 0.0122% of the antioxidant Anox 330 (1,3,5-trimethyl-2,4,6-tris(3,5-di-tert-4-hydroxybenzyl)benzene) under nitrogen atmosphere at ⁇ 215°C.
  • MAA:triglyceride was 2:1.
  • MAA was added in 16 portions. The first 8 portions of 407.5g MAA were added every 15 minutes, while the last 8 portions of 1.63kg were added every 30 minutes.
  • Sized papers were tested by making Cobb tests; sheets of paper with the use of the new sizing agents from Example 1 or 2 were produced. Sheets were formed on a Rapid-Kothen sheet former with grounded cellulose (30°SR, 2% dry content, 30% short fibre and 70% long fibre from bleached kraft pulp).
  • 1 % of the tested sizing agent was emulsified in a polymer solution (4% HI-CAT 5103A cationic starch in water) - with an Ultra Turrax for 2 minutes at 10 000 rpm at 70°C. This emulsion was diluted 1:10 with deionized water and 3-4.7 ml ( ⁇ 1.3-2.0 kg/t) of this dilution was added to approx.
  • 190g respectively 240g paper stock (diluted from 2% stock solution, containing 1% fibers and 0.25% grounded calcium carbonate (GCC) at room temperature. Afterwards following chemicals were added to the slurry to help in sizing: 1 ml Alum (1%) and 4.6 ml Fennopol (0.01 %, cationic polymer, K 3400R from Kemira Oyj). Then the sheet was formed at room temperature. The freshly prepared sheet was dried in a drum dryer at ⁇ 115°C for 40s, and at 125°C for 10 min in an oven. Subsequently, the water uptake in 60 seconds was determined according to the Cobb test, German Industrial Standard DIN 53132. The results are presented in Fig 1 .
  • 1 g size according to example 4 was emulsified in 99 g starch solution (4% High Cat 5103A) at 70°C, 10 000 rpm, for 2 min.
  • This emulsion was diluted 1:10, 1.5-3ml ( ⁇ 0.6-1.2 kg size/t of paper) of it was added to approx. 190g of the paper stock (containing 1 % fibers and 0.25% GCC) at 45°C, 1.5 ml Alum (1 %) and 4.6 ml Fennopol K3400 R (0.01 %) were added after the size emulsion.
  • the sheet was prepared and dried in a drum dryer once. From the measured Cobb values presented in Fig. 2 can be seen that the blends have a sizing efficiency as good as ASA alone.
  • Emulsions were diluted 1:10 and 2.5 ml ( ⁇ 1.1 kg/t) was added to approx. 165g paper stock (containing 1% fibers and 0.25% GCC) at room temperature, 1.7 ml Alum (1%) and 4.6 ml Fennopol K3400 R (0.01 %) were added. Then the sheets were prepared and dried in a drum dryer once and for 10min at 125°C in an oven. From the measured Cobb values presented in Fig. 3 can be seen that blends of FAA and SOHO have better sizing efficiency than both pure sizing agents. It clearly proves the synergy between FAA and SOHO, which cannot be seen in the ASA - FAA blends.
  • the reaction according to example 14 was made by altering the reaction time. Viscosity, polymer content, residual oil, and MAA:triglyceride ratio (R) in the maleated vegetable oil were measured after reaction and distillation.
  • R was calculated using the saponification number method.
  • the viscosity was measured with a rotational - viscometer (Anton Paar GmbH, Austria, RHEOLAB MC1) at 20°C and a shear rate of 50s-1 from the table 6 can be seen that viscosity increases with the increasing reaction time.
  • Table 6 Time [min]
  • Polygraphix 2500 is a market established anionic surface size based on styrene acrylate copolymer.
  • the used paper was unsized copy paper (Grammage 135g/m 2 ).

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  • Paper (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
EP09157679A 2009-04-09 2009-04-09 Produit d'encollage du papier Withdrawn EP2239369A1 (fr)

Priority Applications (16)

Application Number Priority Date Filing Date Title
EP09157679A EP2239369A1 (fr) 2009-04-09 2009-04-09 Produit d'encollage du papier
PL10717671T PL2417297T3 (pl) 2009-04-09 2010-04-09 Produkt do zaklejania papieru
CN2010800156170A CN102388181B (zh) 2009-04-09 2010-04-09 用于纸张施胶的产品
ES10717671T ES2747791T3 (es) 2009-04-09 2010-04-09 Producto para aprestar papel
MX2011010653A MX2011010653A (es) 2009-04-09 2010-04-09 Producto para encolado de papel.
EP10717671.1A EP2417297B1 (fr) 2009-04-09 2010-04-09 Produit d'encollage du papier
RU2011141340/04A RU2538957C2 (ru) 2009-04-09 2010-04-09 Продукт для проклеивания бумаги
CA2756148A CA2756148C (fr) 2009-04-09 2010-04-09 Produit pour l'encollage de papier
BRPI1016127A BRPI1016127B1 (pt) 2009-04-09 2010-04-09 "produto para engomagem de papel."
JP2012504042A JP5737814B2 (ja) 2009-04-09 2010-04-09 紙のサイズ処理用製造物
US13/263,121 US8512521B2 (en) 2009-04-09 2010-04-09 Product for the sizing of paper
KR1020117026730A KR101736413B1 (ko) 2009-04-09 2010-04-09 지류 사이징용 제품
PCT/FI2010/050288 WO2010116044A1 (fr) 2009-04-09 2010-04-09 Produit pour l'encollage de papier
AU2010233629A AU2010233629B2 (en) 2009-04-09 2010-04-09 Product for the sizing of paper
CL2011002504A CL2011002504A1 (es) 2009-04-09 2011-10-07 Emulsion de encolado de papel que comprende agente de encolado de aceite vegetal maleatado en donde por lo menos 50% en peso de acidos grasos totales de los trigliceridos son monoinsaturados; agente de encolado de papel, proceso de preparacion de emulsion de encolado de papel; y uso de dicha emulsion.
ZA2011/08224A ZA201108224B (en) 2009-04-09 2011-11-09 Product for the sizing of paper

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP09157679A EP2239369A1 (fr) 2009-04-09 2009-04-09 Produit d'encollage du papier

Publications (1)

Publication Number Publication Date
EP2239369A1 true EP2239369A1 (fr) 2010-10-13

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ID=41058957

Family Applications (2)

Application Number Title Priority Date Filing Date
EP09157679A Withdrawn EP2239369A1 (fr) 2009-04-09 2009-04-09 Produit d'encollage du papier
EP10717671.1A Active EP2417297B1 (fr) 2009-04-09 2010-04-09 Produit d'encollage du papier

Family Applications After (1)

Application Number Title Priority Date Filing Date
EP10717671.1A Active EP2417297B1 (fr) 2009-04-09 2010-04-09 Produit d'encollage du papier

Country Status (15)

Country Link
US (1) US8512521B2 (fr)
EP (2) EP2239369A1 (fr)
JP (1) JP5737814B2 (fr)
KR (1) KR101736413B1 (fr)
CN (1) CN102388181B (fr)
AU (1) AU2010233629B2 (fr)
BR (1) BRPI1016127B1 (fr)
CA (1) CA2756148C (fr)
CL (1) CL2011002504A1 (fr)
ES (1) ES2747791T3 (fr)
MX (1) MX2011010653A (fr)
PL (1) PL2417297T3 (fr)
RU (1) RU2538957C2 (fr)
WO (1) WO2010116044A1 (fr)
ZA (1) ZA201108224B (fr)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2018178513A1 (fr) * 2017-03-27 2018-10-04 Kemira Oyj Procédé de fabrication de papier ou de carton et produit de papier ou de carton
EP3814571A4 (fr) * 2018-06-26 2022-03-23 Solenis Technologies, L.P. Compositions et procédés destinés à améliorer les propriétés de matériaux lignocellulosiques

Families Citing this family (6)

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Publication number Priority date Publication date Assignee Title
US8852400B2 (en) 2010-11-02 2014-10-07 Ecolab Usa Inc. Emulsification of alkenyl succinic anhydride with an amine-containing homopolymer or copolymer
US9365979B2 (en) 2014-08-27 2016-06-14 Ecolab Usa Inc. Method of increasing paper surface strength by using polyaluminum chloride in a size press formulation containing starch
CN104805732A (zh) * 2015-05-15 2015-07-29 贺明波 一种苯丙乳液型高效表面施胶剂及其制备方法
CN106917324B (zh) * 2015-12-25 2019-11-08 艺康美国股份有限公司 一种造纸施胶方法及其制备的纸张
US20230062079A1 (en) * 2021-08-31 2023-03-02 Elham Fini Hemp composites
US20230212820A1 (en) * 2021-12-30 2023-07-06 Kemira Oyj High cationic starch as a promoter in akd sizing emulsions

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WO2006002867A1 (fr) 2004-06-29 2006-01-12 Ciba Specialty Chemicals Holding Inc. Produit utilisable pour la fabrication du papier et preparation du produit
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US3855163A (en) 1973-03-08 1974-12-17 Inmont Corp Maleinized fatty acid esters of 9-oxatetracyclo-4.4.1{11 o{11 o{11 {11 undecan-4-ol
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WO2018178513A1 (fr) * 2017-03-27 2018-10-04 Kemira Oyj Procédé de fabrication de papier ou de carton et produit de papier ou de carton
RU2751124C2 (ru) * 2017-03-27 2021-07-08 Кемира Ойй Способ производства бумаги или картона и бумажный или картонный продукт
US11136722B2 (en) 2017-03-27 2021-10-05 Kemira Oyj Method for manufacturing paper or board and paper or board product
AU2018241379B2 (en) * 2017-03-27 2022-09-22 Kemira Oyj Method for manufacturing paper or board and paper or board product
EP3814571A4 (fr) * 2018-06-26 2022-03-23 Solenis Technologies, L.P. Compositions et procédés destinés à améliorer les propriétés de matériaux lignocellulosiques

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AU2010233629B2 (en) 2016-06-09
EP2417297B1 (fr) 2019-06-05
CA2756148C (fr) 2017-02-14
CN102388181A (zh) 2012-03-21
ZA201108224B (en) 2013-01-30
CL2011002504A1 (es) 2012-04-20
ES2747791T3 (es) 2020-03-11
JP5737814B2 (ja) 2015-06-17
RU2011141340A (ru) 2013-05-20
KR20120017036A (ko) 2012-02-27
KR101736413B1 (ko) 2017-05-29
AU2010233629A1 (en) 2011-10-13
CN102388181B (zh) 2013-12-18
MX2011010653A (es) 2011-10-28
JP2012523504A (ja) 2012-10-04
US8512521B2 (en) 2013-08-20
RU2538957C2 (ru) 2015-01-10
EP2417297A1 (fr) 2012-02-15
PL2417297T3 (pl) 2019-11-29
US20120125553A1 (en) 2012-05-24
WO2010116044A1 (fr) 2010-10-14
BRPI1016127B1 (pt) 2019-09-03
BRPI1016127A2 (pt) 2016-11-08

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